US10479799B2ActiveUtilityPatentIndex 61
Solid catalyst for dehydration of mannitol, and method for producing 2, 5-sorbitan and/or isomannide using this catalyst
Est. expiryAug 29, 2036(~10.1 yrs left)· nominal 20-yr term from priority
B01J 29/7007B01J 29/084B01J 2523/00B01J 29/70B01J 29/08Y02P20/584C07B 61/00B01J 29/082C07D 493/04
61
PatentIndex Score
1
Cited by
11
References
12
Claims
Abstract
Provided is a solid acid catalyst which enables the production of isomannide and/or 2,5-sorbitan from mannitol with high yield and high safety at low cost. The mannitol may be derived from a cellulose and/or a hemicellulose. The solid acid catalyst for dehydration contains an acid type β-zeolite and/or a Y type zeolite.
Claims
exact text as granted — not AI-modifiedThe invention claimed is:
1. A solid, dehydration catalyst for producing 2,5-sorbitan and/or isomannide from mannitol comprising an H-type β zeolite and/or a Y-type zeolite.
2. The solid, dehydration catalyst according to claim 1 consisting essentially of the H-type β-zeolite.
3. The solid, dehydration catalyst according to claim 1 consisting essentially of the Y-type zeolite.
4. The solid, dehydration catalyst according to claim 1 , wherein the H-type β-zeolite and/or Y-type zeolite has a Si/Al atomic composition ratio of 10 to 300.
5. The solid, dehydration catalyst according to claim 4 , wherein the Si/Al atomic composition ratio of the H-type β-zeolite and/or Y-type zeolite is 25 to 150.
6. The solid, dehydration catalyst according to claim 5 , wherein the Si/Al atomic composition ratio of the H-type β-zeolite and/or Y-type zeolite is 40 to 100.
7. A process for producing 2,5-sorbitan and/or isomannide from mannitol, comprising the steps of:
(a) adding the solid, dehydration catalyst according to claim 1 to mannitol to obtain a reaction mixture, and
(b) heating the reaction mixture obtained in step (a) to a temperature of 110° C. to 170° C. at ambient pressure or under reduced pressure.
8. The process according to claim 7 , wherein the amount of the solid, dehydration catalyst is 5 to 50% by weight, based on 100% by weight of the mannitol.
9. The process according to claim 7 , wherein the solid, dehydration catalyst consists essentially of the H-type β zeolite, and wherein the process further comprises producing isomannide.
10. The process according to claim 7 , wherein the process further comprises producing isomannide by 1,4-mannitan.
11. The process according to claim 7 , wherein the solid, dehydration catalyst consists essentially of the Y-type zeolite, and wherein the process further comprises producing 2,5-sorbitan.
12. A process for selectively producing isomannide from mannitol or 2,5-sorbitan from mannitol comprising catalytically dehydrating mannitol by use of any of the compositions selected from the group consisting of an H-type β zeolite, a Y-type zeolite or a mixture thereof.Cited by (0)
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